Abstract

The fluid properties of CO 2 injected into geological formations for subsurface storage are strongly affected by the specific formation conditions of pressure, temperature and salinity. Specifically, these conditions affect fluid solubility and density; we investigate their effects on subsurface CO 2 storage efficiency. We compared several common equations-of-state (EOS) and solubility models; their accuracy and applicability are briefly discussed. We also evaluated the effects of gaseous/supercritical CO 2 phase density and mutual solubility, including H 2 O solubility in CO 2 . Results suggest that disparities in phase density estimates by different EOS typically do not translate to large disparities in simulation results because of the low solubility of H 2 O in gaseous/supercritical CO 2 . However, more experimental studies on the solubility of H 2 O in CO 2 are needed, especially at high pressures and temperatures. Simulation results also suggest that formations at higher temperatures are less efficient for CO 2 storage than equivalent formations at lower temperatures. We evaluated aqueous- CO 2 solution density at a broad range of pressure and temperature conditions using different equations-of-state. Results indicate that CO 2 -dissolution in brine at high temperatures (>120 °C) may reduce mass density to values lower than the original brine density, nullifying the primary advantage of the dissolution trapping mechanism. This concept, equal density temperature, is proposed here for the first time. In certain scenarios with temperatures greater than the equal density temperature, CO 2 can exsolve (escape the aqueous phase) and be subject to buoyancy-driven migration (and potential escape from the formation) associated with separate phase CO 2 . Simulation results are very sensitive to the density models selected. Predictions of CO 2 -enriched brine migration using different models can yield contradictory results.

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